ScholarWorks@KOREA RESEARCH INSTITUTE OF SHIPS & OCEAN ENGINEERING: Lee, Ho saeng

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Lee, Ho saeng (이호생)

친환경해양개발연구본부 (해수에너지연구센터)

Research Area: 해수열에너지 이용, Utilization of Seawater Thermal energy

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OTEC:15||Ocean thermal energy conversion:11||해수온도차발전:9||Ocean Thermal Energy Conversion:7||Performance analysis:6||Deep seawater:6||Ejector:5||Adsorption desalination:4||유기랭킨사이클:4||Membrane distillation:4||Seawater desalination:4||해양온도차발전:4||성능분석:4||Ocean thermal energy conversion (OTEC):4||ORC:3||j factor:3||Performance evaluation:3||Motive pump:3||Liquidvapor ejector:3||Heat pump:3||Vacuum membrane distillation:3||Closed cycle:3||f factor:3||Waste heat:3||이젝터:3||closed cycle:2||Microbubble generator:2||Indirect desalination cycle:2||성능계수:2||R245fa:2||ocean thermal energy conversion:2||OTEC Power Cycle:2||시스템효율:2||Entrainment ratio:2||심층수:2||R717:2||Mixed refrigerant:2||해수담수화:2||R744:2||System efficiency:2||해양심층수:2||Computational Fluid Dynamics:2||Ocean Thermal Energy Conversion(OTEC):2||해양온도차 발전시스템(Ocean Thermal Energy Conversion(OTEC)):2||Rankine cycle:2||Kalina cycle:2||Open cycle:2||1stage cycle:2||Concentrated seawater:2||Operating pressure:2||Riser:2||Turbine:2||Exergy analysis:2||2stage cycle:2||COP:2||Twophase flow:2||Heating cycle:2||Deep seawater 해양심층수:2||농축수:2||HighEfficiency:2||Seawater Thermal Energy:2||Airconditioning:2||Desalination:2||Seawater heat pump:2||Humidificationdehumidification:2||Brine salinity:2||Permeation flux enhancement:2||Coefficient of performance:2||Plate heat exchanger:2||Preliminary design:2||Adsorption isotherms:2||터빈:2||Floating structure:1||Floating wave energy converter:1||Flow Analysis:1||Freezing desalination:1||Fresh water generator:1||Fuel consumption:1||Functional adsorbent material:1||Generator 재생기:1||Geothermal water:1||Global Warming Potential:1||Green economies:1||Green energy:1||Green hydrogen:1||Green olympic blue ice (GOBI) rink:1||HCFC22:1||Hard water:1||Hazard analysis:1||Head:1||Heat Pump:1||Heat Sink:1||Heat and mass transfer:1||Heat pump control:1||Heat pumps:1||Heat source:1||Heat storage tank:1||Heat transfer:1||Heat transfer coefficient:1||Heavy fuel oil:1||Hot Waste Water:1||Hot wastewater:1||Humidifier:1||Hybrid:1||Hydroponics:1||Ice productivity:1||Initial time lag (ITL):1||Internal heat exchanger(IHX):1||Internal rate of return:1||Jacket cooling water:1||Keulegan Carpenter number:1||KeuleganCarpenter number:1||Knudsen diffusion:1||LOTEC:1||LNG:1||Law of similarity:1||Liquefaction cycle:1||Liquidvapor Separator:1||Lowgrade heat utilization:1||Lower heating value:1||Machine Learning:1||Mass and heat transfer:1||Materialgap membrane distillation:1||Membrane crystallization:1||Membrane filtration:1||Microfin tube:1||Mineral:1||Minimal liquid discharge:1||Mixed Refrigerant:1||Mixed working fluids:1||Mooring line 계류선:1||Mooring system:1||Multi Effect Distillation:1||Multi Stage Flash:1||Multi Stage Reheater & Recuperator Cycle:1||Multi Stage Reheater Cycle:1||MultiEffect Distillation:1||Multipeak frequency:1||Multistage direct contact membrane distillation:1||Multistaged Reheater Regeneration Cycle:1||Multiple condensers:1||Multiplebed effect:1||Nano filtration:1||Nano filtration membrane:1||Natural refrigerants:1||Net power:1||Net present value:1||Nickel Doped Indium Zinc Oxide (NIZO):1||Nonequilibrium Model:1||Numerical Analysis:1||Numerical analysis:1||ODA(Official Development Aids):1||OTEC (Ocean Thermal Energy Conversion) cycle:1||OTEC power cycle:1||Ocean Geothermal Power Generation:1||Ocean Thermal Energy Conversion (OTEC):1||Ocean Thermal Energy Conversion(OTEC) Power Cycle:1||Ocean thermal energy conversio:1||Open cycle ocean thermal energy conversion (OTEC):1||OpenFOAMbased CFD:1||Optical Transparent:1||Optimal AD sequence:1||Optimization:1||Organic Rankine Cycle:1||Organic Rankine Cycle (ORC):1||Organic Rankine cycle:1||Organic rankine cycle(ORC):1||Ozone Depletion Potential:1||POSS Amine:1||PVRO Desalination system:1||Performance Analysis:1||Performance Evaluation:1||Performance comparison:1||Pilot experiment:1||Plate heat exchangers:1||Pressure drop:1||Pretension 초기장력:1||Primary production 기초생산:1||Pump:1||Pure refrigerant:1||R32:1||R32/R1270 mixture:1||R32/R152a:1||R32/R290 Mixture:1||R717 (ammonia):1||Radial Turbine:1||Radial outflow turbine:1||Rankin cycle:1||Reduced Pressure Evaporation:1||Refrigerant flow Rate:1||Refrigerant leakage:1||Refrigerant mixture:1||Regasification:1||Regenerate Cellulose:1||Reverse osmosis:1||Reverse osmosis brine:1||Riser loss:1||SSUA(Sustainable Seawater Utilization Academy):1||SWAC:1||Safety analysis:1||Safety analysis 안전성해석:1||Salinity:1||Saturated Vapor Pressure:1||Sea water air conditioning (SWAC):1||Seawater:1||Seawater air conditioning:1||Seawater concentration:1||Seawater heat source:1||Seawater heatpump:1||Seawater plant:1||Seawater utilization technologies:1||Sequence control:1||Ship Waste Heat:1||Ship waste heat:1||Siphon effect:1||Sol Gel Process:1||Solar energy:1||Solar thermal collection:1||Specific Heat:1||Spray Nozzle:1||Steady State cycle:1||Steam flow fraction:1||Subcooling degree:1||Subsystem risk analysis:1||Supercritical working fluid:1||Surface Water flow Rate:1||Surface seawater:1||Surface water temperature:1||Switching interval:1||Tandem heat pump:1||Thermal Conductivity:1||Thermal Diffusivity:1||Thermal Vapor Compression:1||Thermal conductivity:1||Thermal energy conversion:1||Thermodynamic system analysis:1||Thermodynamicschemical quality nexus:1||Thermoeconomics:1||Thermoelectric generation:1||Top excitation:1||Total Work:1||Transparent Conducting Oxide (TCO):1||Turbine Generator:1||Turbine generator:1||Turbine pressure ratio:1||Two Phase:1||Two phase flow:1||T열적 증기 압축기:1||Unit cost of electricity:1||Unused heat:1||VIV:1||Vacuum Membrane Distillation:1||Vacuum pump:1||Vaporization heat:1||Vessel:1||Volume flow ratio:1||Vortexinduced vibration:1||Waste heat recovery:1||Waste heat recovery system:1||Waste heat 폐열:1||Watergap membrane distillation:1||Wind turbine:1||Wireless sensor:1||Working Fluid:1||Working fluid:1||air conditioning system using seawater:1||ceramic coating:1||deep sea water:1||frequency modulation:1||internal rate of return:1||large diameter riser:1||net present value:1||numerical analysis:1||open cycle:1||performance analysis:1||plate heat exchanger:1||proportionalintegraldifferential controller:1||structural health monitoring:1||subcritical cycle:1||surface water:1||turbine efficiency:1||vaporvapor ejector:1||간접 냉동법 담수화:1||간접식 냉동법 담수화사이클:1||감압증발:1||개방형:1||경제성(Lifecyclecost):1||계류시스템:1||고경도수:1||고효율:1||고효율(high efficiency):1||국내적용:1||급액가열기:1||기계 학습:1||기화냉열:1||끓는점:1||나노여과:1||나노여과 막:1||난방사이클:1||내부 수익률:1||냉매 유량:1||농도:1||다단 증발식:1||다단재열사이클:1||다단재열재생사이클:1||다단재열재생사이틀:1||다중효용담수화:1||단일냉매:1||동적 사이클:1||동적사이클:1||랭킨사이클:1||막여과:1||미활욜열:1||배출수:1||부유식 파력발전장치:1||분사 노즐:1||분산 상 모델:1||비교연구:1||비평형 모델:1||빙상경기장(Icerink):1||사이펀 효과:1||상사법칙:1||선박:1||선박폐열:1||선박폐열발전:1||성능 비교(Performance comparison):1||성능(Performance):1||성능분석(Performance analysis):1||순 현재 가치:1||순수 발전량:1||습냉매(Wet refrigerant):1||시스템 효율:1||신재생에너지(Renewableenergy):1||심층수 유량:1||안전성 해석:1||암모니아:1||암모니아 운반선:1||암모니아(ammonia):1||액증기 이젝터:1||액화천연가스:1||양정:1||엑서지 분석:1||엔진 냉각수:1||역삼투:1||연료 소비량:1||열침:1||열펌프:1||염도:1||예비 설계:1||오존층파괴지수:1||외향반경류형터빈:1||유기 랭킨 사이클:1||유기랭킨사이클의 사이클 종류:1||유동해석:1||작동부 펌프:1||작동유체:1||작동유체(Working fluid):1||재기화:1||저위 발열량:1||적용방안(Application):1||전기투석:1||전산유체역학:1||정적사이클:1||조수기:1||중유:1||증기증기 이젝터(Vaporvapor ejector):1||증기증기 이젝터(Vaprovapor ejector):1||증류:1||증발열량(Evaporation capacity):1||지구온난화지수:1||직접냉방:1||진공 펌프:1||진공막증류:1||질량유량비:1||채널 간격:1||체적유량비:1||초기 설계:1||최적화:1||칼리나 사이클:1||칼리나사이클:1||터빈 발전기:1||터빈발전기:1||파일럿플랜트:1||판형열교환기:1||펌프:1||폐쇄 사이클:1||폐쇄형:1||폐열:1||폐열회수:1||포화증기압:1||표층수 유량:1||표층수온:1||플래시 증발:1||항온조:1||해수:1||해수 농축:1||해수 담수화:1||해수냉난방:1||해수열원(Seawaterheatsource):1||해수온도차발전. 지열수:1||해수히트펌프:1||해양온도차 발전 사이클:1||해양온도차 발전사이클:1||해양온도차발전사이클(OTEC):1||해양지열발전:1||혼합냉매:1||혼합작동유체:1||효율(Efficiency):1||히트펌프:1||히트펌프시스테:1||1단 사이클:1||2단 사이클:1||2상 유동:1||Adsorbent:1||Adsorption Desalination:1||Adsorption isotherm:1||Adsorptive Desalination:1||Airconditioners:1||Alternative Working Fluid:1||Alternative working fluid:1||Ammonia carrier:1||Antimicrobial:1||Artificial upwelling system in floating type 부유식 인공용승시스템:1||Availability:1||Boiling Point:1||Bosanquet equation:1||Brine treatment:1||Brownian diffusion:1||CO2:1||Capacity building:1||Cascade cycle:1||Cellulose:1||Channel space:1||Chiller:1||Closed type ocean thermal ener:1||Closedtype ocean thermal energy conversion 폐쇄형 해양온도차발전:1||Coefficient of Performance:1||Combined Brownian/Knudsen diffusion:1||Comparative study:1||Concentration:1||Concept design:1||Condensation heat transfer:1||Condenser Pressure:1||Control logic:1||Cooler:1||Cooling heat transfer:1||Corrugated PlateandFrame Heat Exchanger:1||Cycle Type of ORC:1||DOTEC Cycle:1||Deep Ocean Water:1||Deep Water flow Rate:1||Deep ocean water:1||Dehumidifier:1||Desalination Plant:1||Design 설계:1||Direct cooling:1||Discrete Phase Model:1||Distillation:1||Domestic applicability:1||Drained deep seawater:1||Dual system of coolingthermal energy conversion:1||Dualuse OTEC:1||Dynamic Cycle:1||Dynamic cycle:1||EPOTEC cycle:1||Effective mean molecular speed:1||Efficiency:1||Effusion:1||Effusion phenomena:1||Electrodialysis:1||Environmentfriendly working fluids:1||Exergy Analysis:1||Expansion valve:1||Experimental study:1||Extreme value analysis 극한해석:1||FDM:1||Feed liquid heater:1||Filtered seawater:1||Fisheries resource 어족자원:1||Flash Evaporation:1||Flash evaporator:1||

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